Naphthoxazine benzoxazine-based monomer, polymer thereof, electrode for fuel cell including the polymer, electrolyte membrane for fuel cell including the polymer, and fuel cell using the electrode

CROSS-REFERENCE TO RELATED APPLICATIONS

0001This is a divisional application of U.S. application Ser. No. 12/262,854, filed Oct. 31, 2008, now U.S. Pat. No. 8,188,210, issued May 29, 2012, which claims the benefit of Korean Patent Application No. 10-2007-0111587, filed on Nov. 2, 2007 and Korean Patent Application No. 10-2008-0099351, filed on Oct. 9, 2008, in the Korean Intellectual Property Office, the disclosures of which are incorporated herein by reference.

BACKGROUND OF THE INVENTION

00021. Field of the Invention

0003One or more embodiments of the present invention relate to a naphthoxazine benzoxazine-based monomer, a polymer thereof, an electrode for a fuel cell including the polymer, an electrolyte membrane for a fuel cell including the polymer, and a fuel cell using the electrode.

00042. Description of the Related Art

0005Fuel cells, which use a polymer electrolyte membrane as an electrolyte, operate at a relatively low temperature and can be small in size. Thus, fuel cells may be used as power sources in electric vehicles or distributed generation systems for homes. As a polymer electrolyte membrane used in polymer electrolyte fuel cells, a perfluorocarbonsulfonic acid-based polymer membrane such as NAFION (registered trademark) has been used.

0006However, such polymer electrolyte membranes typically need water to provide proton conduction abilities, and thus the polymer electrolyte membranes typically need to be humidified. In addition, to enhance cell system efficiencies, it may be necessary to operate polymer electrolyte membranes at a high temperature of at least 100° C. However, the moisture in polymer electrolyte membranes may evaporate at this temperature, and the polymer electrolyte membranes may not function properly as a solid electrolyte.

0007To address those problems in the art, non-humidified electrolyte membranes that can operate at a high temperature of at least 100° C. under nonhumidified conditions have been developed. For example, U.S. Pat. No. 5,525,436 discloses polybenzimidazole doped with a phosphoric acid, and the like as a material constituting non-humidified electrolyte membranes.

0008In addition, in cells that operate at a low temperature, such as cells using a perfluorocarbonsulfonic acid-based polymer membrane, to prevent gas diffusion in electrodes due to water (formation water) that is produced as electricity is generated in an electrode, particularly a cathode, electrodes using polytetrafluoroethylene (PTFE) as a waterproof agent to have hydrophobic properties have been widely used (see, for example, Japanese Patent Laid-Open Publication No. hei 05-283082).

0009In addition, phosphoric acid type fuel cells operating at a high temperature of 150 to 200° C. use a liquid phosphoric acid as an electrolyte. However, a large amount of the liquid phosphoric acid is present in electrodes, which interferes with gas diffusion. Therefore, an electrode catalyst layer that is formed by adding polytetrafluoroethylene (PTFE) as a waterproof agent to an electrode catalyst, and which can prevent fine pores in electrodes from being clogged by a phosphoric acid, has been used.

0010In addition, in fuel cells using a polybenzimidazole (PBI) electrolyte membrane, which retains phosphoric acid as a nonhumidified electrolyte at a high temperature, to reduce contact between electrodes and the electrolyte membrane, a method of impregnating electrodes with a liquid phosphoric acid has been tried and a method of increasing a loading amount of metal catalysts has been tried. However, such fuel cells have not exhibited improved properties, and thus there is a need for improvement.

0011In addition, when air is supplied to a cathode when a solid polymer electrolyte doped with phosphoric acid is used, the fuel cell requires an aging time of about 1 week even if the composition of the cathode is optimized. By supplying oxygen to the cathode instead of air, performance of the cathode can be improved and aging time can also be reduced. However, the need to supply of oxygen to the cathode is an obstacle in realizing widespread use of the cathode.

SUMMARY OF THE INVENTION

0012One or more embodiments of the present invention include a naphthoxazine benzoxazine-based monomer, a polymer thereof, an electrode for a fuel cell including the polymer, an electrolyte membrane for a fuel cell including the polymer, and a fuel cell which includes an electrode for a fuel cell formed using the polymer thereof, thereby having improved cell performance.

0013Additional aspects and/or advantages will be set forth in part in the description which follows and, in part, will be apparent from the description, or may be learned by practice of the invention.

0014According to an embodiment of the present invention, there is provided a naphthoxazine benzoxazine-based monomer represented by Formula 1 below:

0015<chemistry id="CHEM-US-00003" num="00003"><img file="US8551669B2_D0001.tif" /></chemistry>

0016wherein R₂and R₃or R₃and R₄are linked to each other to form a group represented by Formula 2 below, and

0017R₅and R₆or R₆and R₇are linked to each other to form a group represented by Formula 2 below,

0018<chemistry id="CHEM-US-00004" num="00004"><img file="US8551669B2_D0002.tif" /></chemistry><br /> wherein, in Formula 2, R₁is a substituted or unsubstituted C₁-C₂₀alkyl group, a substituted or unsubstituted C₁-C₂₀alkoxy group, a substituted or unsubstituted C₂-C₂₀alkenyl group, a substituted or unsubstituted C₂-C₂₀alkynyl group, a substituted or unsubstituted C₆-C₂₀aryl group, a substituted or unsubstituted C₆-C₂₀aryloxy group, a substituted or unsubstituted C₇-C₂₀arylalkyl group, a substituted or unsubstituted C₂-C₂₀heteroaryl group, a substituted or unsubstituted C₂-C₂₀heteroaryloxy group, a substituted or unsubstituted C₂-C₂₀heteroarylalkyl group, a substituted or unsubstituted C₄-C₂₀carbocycle group, a substituted or unsubstituted C₄-C₂₀carbocyclic alkyl group, a substituted or unsubstituted C₂-C₂₀heterocycle group, or a substituted or unsubstituted C₂-C₂₀heterocyclic alkyl group,

0019in Formula 2, * represents the bonding position of R₂and R₃, R₃and R₄, R₅and R₆, or R₆and R₇of Formula 1, and

0020R₂or R₄that does not form a group of Formula 2 is hydrogen and R₅or R₇that does not form a group of Formula 2 is hydrogen.

0021According to an embodiment of the present invention, there is provided a polymer of a naphthoxazine benzoxazine-based monomer which is a polymerization product of the naphthoxazine benzoxazine-based monomer described above or a polymerization product of the naphthoxazine benzoxazine-based monomer described above and a crosslinkable compound.

0022According to an embodiment of the present invention, there is provided an electrode for a fuel cell, the electrode comprising a catalyst layer comprising the polymer of the naphthoxazine benzoxazine-based monomer.

0023According to an embodiment of the present invention, there is provided an electrolyte membrane for a fuel cell, the electrolyte membrane comprising the polymer of the naphthoxazine benzoxazine-based monomer.

0024According to an embodiment of the present invention, there is provided a fuel cell comprising a cathode; an anode; and an electrolyte membrane interposed between the cathode and the anode, wherein at least one of the cathode and the anode comprises a catalyst layer comprising the polymer of the naphthoxazine benzoxazine-based monomer described above or wherein the electrolyte membrane comprises the polymer of the naphthoxazine benzoxazine-based monomer described above.

0025Additional aspects and/or advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.

BRIEF DESCRIPTION OF THE DRAWINGS

0026These and/or other aspects and advantages will become apparent and more readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

0027<figref idref="DRAWINGS">FIG. 1</figref> is a graph showing thermogravimetric analysis (TGA) results of a compound prepared in Synthesis Example 1, a compound prepared in Synthesis Example 4, and t-BuPh-a prepared in Reference Example 1;

0028<figref idref="DRAWINGS">FIG. 2</figref> is a graph showing a change in voltage with respect to time of fuel cells prepared in Example 1 and Comparative Example 1;

0029<figref idref="DRAWINGS">FIG. 3</figref> is a graph showing a change in cell potential with respect to current density of fuel cells prepared in Examples 1 and 2 and Comparative Example 1;

0030<figref idref="DRAWINGS">FIGS. 4 through 9</figref> are graphs showing nuclear magnetic resonance (NMR) spectra of target materials prepared in Synthesis Examples 1 through 5, respectively;

0031<figref idref="DRAWINGS">FIGS. 10 and 11</figref> are graphs showing TGA results of 16DHN3AP and 27DHN34DFA and TGA results of a polymer of 16DHN3AP and PBI and a polymer of 27DHN34DFA and PBI prepared in Synthesis Examples 7 and 8, respectively;

0032<figref idref="DRAWINGS">FIG. 12</figref> is a graph showing voltage characteristics according to current density of a fuel cell prepared in Example 6;

0033<figref idref="DRAWINGS">FIG. 13</figref> is a graph showing a change in cell voltage according to time of a fuel cell prepared in Example 6;

0034<figref idref="DRAWINGS">FIGS. 14 and 15</figref> are graphs respectively showing conductivity according to temperature and phosphoric acid doping level of electrolyte membranes prepared in Examples 6 through 9;

0035<figref idref="DRAWINGS">FIG. 16</figref> is a graph showing a solid NMR spectrum of a polymer of 27DHN34DFA and PBI according to an embodiment of the present invention; and

0036<figref idref="DRAWINGS">FIG. 17</figref> is a graph showing cell voltage characteristics according to current density of fuel cells prepared in Example 10 and Comparative Example 2.

DETAILED DESCRIPTION OF THE EMBODIMENTS

0037Reference will now be made in detail to the present embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the like elements throughout. The embodiments are described below in order to explain the present invention by referring to the figures.

0038A naphthoxazine benzoxazine-based monomer according to an embodiment of the present invention is represented by Formula 1 below:

0039<chemistry id="CHEM-US-00005" num="00005"><img file="US8551669B2_D0003.tif" /></chemistry>

0040wherein R₂and R₃or R₃and R₄are linked to each other to form a group represented by Formula 2 below, and

0041R₅and R₆or R₆and R₇are linked to each other to form a group represented by Formula 2 below.

0042<chemistry id="CHEM-US-00006" num="00006"><img file="US8551669B2_D0004.tif" /></chemistry>

0043In Formula 2, R₁is a substituted or unsubstituted C₁-C₂₀alkyl group, a substituted or unsubstituted C₁-C₂₀alkoxy group, a substituted or unsubstituted C₂-C₂₀alkenyl group, a substituted or unsubstituted C₂-C₂₀alkynyl group, a substituted or unsubstituted C₆-C₂₀aryl group, a substituted or unsubstituted C₆-C₂₀aryloxy group, a substituted or unsubstituted C₇-C₂₀arylalkyl group, a substituted or unsubstituted C₂-C₂₀heteroaryl group, a substituted or unsubstituted C₂-C₂₀heteroaryloxy group, a substituted or unsubstituted C₂-C₂₀heteroarylalkyl group, a substituted or unsubstituted C₄-C₂₀carbocyclic group, a substituted or unsubstituted C₄-C₂₀carbocyclic alkyl group, a substituted or unsubstituted C₂-C₂₀heterocyclic group, or a substituted or unsubstituted C₂-C₂₀heterocyclic alkyl group,

0044in Formula 2, * represents the bonding position of R₂and R₃, R₃and R₄, R₅and R₆, or R₆and R₇, respectively, of Formula 1, and

0045R₂or R₄that does not form a group of Formula 2 is hydrogen and R₅or R₇that does not form a group of Formula 2 is hydrogen.

0046As non-limiting examples, R₁may be one selected from groups represented by the following formulae.

0047<chemistry id="CHEM-US-00007" num="00007"><img file="US8551669B2_D0005.tif" /></chemistry>

0048As non-limiting examples, the naphthoxazine benzoxazine-based monomer may be at least one selected from compounds represented by Formulae 3 through 5.

0049<chemistry id="CHEM-US-00008" num="00008"><img file="US8551669B2_D0006.tif" /></chemistry>

0050In Formulae 3 through 5, R₁may be a group as defined in Formula 1, and, as non-limiting examples, may be selected from groups represented by the following formulae.

0051<chemistry id="CHEM-US-00009" num="00009"><img file="US8551669B2_D0007.tif" /></chemistry>

0052The naphthoxazine benzoxazine-based monomer according to aspects of the present invention has structural stiffness due to an increase in crosslinked sites. In addition, when the naphthoxazine benzoxazine-based monomer is used in forming an electrode for a fuel cell, fluorine, a fluorine-containing functional group, or a pyridine functional group is introduced into the monomer as described above, and thus oxygen transmittance and an amount of phosphoric acid injected into the electrode can be increased and thermal resistance and resistance to phosphoric acid can be obtained at the same time.

0053In addition, the naphthoxazine benzoxazine-based monomer according to an embodiment of the present invention includes a naphthoxazine group that can maximize a hydrogen bond in a molecule and a hydrogen bond between molecules, and thus, when the naphthoxazine benzoxazine-based monomer is co-polymerized with a crosslinkable compound, the number of crosslinkable sites increases. Thus, by using the naphthoxazine benzoxazine-based monomer, a fuel cell that can have excellent thermal stability and durability at an operating temperature, and thereby having a long lifetime, can be prepared.

0054In addition, when the naphthoxazine benzoxazine-based monomer is simultaneously used in an electrode and an electrolyte membrane, the compatibility of an interface between the electrolyte membrane and the electrode is enhanced. Thus, the performance of a fuel cell can be maximized.

0055The naphthoxazine benzoxazine-based monomer represented by Formula 1 may be one selected from compounds represented by Formulae 6 through 11.

0056<chemistry id="CHEM-US-00010" num="00010"><img file="US8551669B2_D0008.tif" /></chemistry>

0057Hereinafter, a method of preparing the naphthoxazine benzoxazine-based monomer of Formula 1 according to aspects of the present invention will be described. As an embodiment of the present invention, a method of preparing the compounds represented by Formulae 3 through 5 will now be described; however, the other compounds described above can be synthesized in a manner similar to the preparation method described herein.

0058Referring to Reaction Scheme 1 below, the compound of Formula 3 can be prepared by heating 1,5-dihydroxynaphthalene (A), p-formaldehyde (B) and an amine compound (C) without a solvent or by adding a solvent to A, B and C and then refluxing the mixture, and thereafter working up the resultant. Referring to Reaction Schemes 2 and 3, the compound of Formula 4 and the compound of Formula 5 can be prepared in the same manner as in Reaction Scheme 1, except that 1,6-dihydroxynaphthalene (A′) or 2,7-dihydroxynaphthalene (A″) are used instead of 1,5-dihydroxynaphthalene (A).

0059<chemistry id="CHEM-US-00011" num="00011"><img file="US8551669B2_D0009.tif" /></chemistry>

0060<chemistry id="CHEM-US-00012" num="00012"><img file="US8551669B2_D0010.tif" /></chemistry>

0061<chemistry id="CHEM-US-00013" num="00013"><img file="US8551669B2_D0011.tif" /></chemistry>

0062In Reaction Schemes 1 through 3, R₁may be selected from the same groups represented by the following formulae as defined in Formulae 3 through 5.

0063<chemistry id="CHEM-US-00014" num="00014"><img file="US8551669B2_D0012.tif" /></chemistry>

0064The solvent used in the reactions described above may be 1,4-dioxane, chloroform, dichloromethane, THF, or the like. The heating temperature is adjusted to a temperature range that can reflux the solvent, such as, for example, a range of 80 to 110° C., or more specifically, about 110° C.

0065As a non-limited embodiment of the working-up process, the resultant reaction mixture is washed with an aqueous 1N NaOH solution and water and dried using a drier such as magnesium sulfate, and then the resultant is filtered and evaporated under reduced pressure in order to remove the solvent from the resultant, and dried to obtain a target material.

0066Non-limiting examples of the C₁-C₂₀alkyl group” include methyl, ethyl, propyl, isobutyl, sec-butyl, pentyl, iso-amyl, hexyl, or the like. The C₁-C₂₀alkyl group may be unsubstituted, or at least one hydrogen atom of the alkyl group may be substituted with a halogen atom such as fluorine and chlorine, a C₁-C₂₀alkyl group substituted with a halogen atom (such as, for example, CCF₃, CHCF₂, CH₂F, CCl₃, and the like), a hydroxyl group, a nitro group, a cyano group, an amino group, an amidino group, hydrazine, hydrazone, a carboxyl group or a salt thereof, a sulfonic acid group or a salt thereof, a phosphoric acid or a salt thereof, a C₁-C₂₀alkyl group, a C₂-C₂₀alkenyl group, a C₂-C₂₀alkynyl group, a C₁-C₂₀heteroalkyl group, a C₆-C₂₀aryl group, a C₅-C₂₀arylalkyl group, a C₆-C₂₀heteroaryl group, a C₁-C₂₀heterocyclic group, or a C₆-C₂₀heteroarylalkyl group.

0067The term “aryl group” as used herein refers to a C₆-C₂₀carbocyclic aromatic system containing at least one ring, wherein the rings can be pendantly attached to each other or fused with each other. The term “aryl,” as used alone or in combination with other terms, refers to an aromatic radical, such as, for example, phenyl, naphthyl, tetrahydronaphthyl, or the like. The aryl group may be unsubstituted or at least one hydrogen atom of the aryl group may be substituted with a substituent described above with respect to the alkyl group.

0068As non-limiting examples, the aryloxy group may be a phenoxy group, a naphthyloxy group, a tetrahydronaphthyloxy group, or the like. The aryloxy group may be unsubstituted or at least one hydrogen atom of the aryloxy group may be substituted with a substituent described above with respect to the alkyl group.

0069The term “heteroaryl group” as used herein refers to a monovalent, monocyclic or bicyclic aromatic bivalent organic compound that contains 1, 2 or 3 hetero atoms selected from the group consisting of N, O, P, and S and has 1 to 20 carbon atoms. As non-limiting examples, the heteroaryl group may be pyrazinyl, furanyl, thienyl, pyridyl, pyrimidinyl, isothiazolyl, oxazolyl, thiazolyl, triazolyl, 1,2,4-thiadiazolyl, or the like. The heteroaryl group may be unsubstituted or at least one hydrogen atom of the heteroaryl group may be substituted with a substituent described above with respect to the alkyl group.

0070As non-limiting examples, the heteroaryloxy group may be pyrazinyloxy, furanyloxy, thienyloxy, pyridyloxy, pyrimidinyloxy, isothiazolyloxy, oxazolyloxy, thiazolyloxy, triazolyloxy, 1,2,4-thiadiazolyloxy, or the like. The heteroaryloxy group may be unsubstituted or at least one hydrogen atom of the heteroaryloxy group may be substituted with the a substituent described above with respect to the alkyl group.

0071The term “heterocyclic group” as used herein refers to a 5 to 10 membered group containing a hetero atom such as nitrogen, sulfur, phosphorus, oxygen, and the like. The heterocyclic group may be unsubstituted or at least one hydrogen atom of the heterocycle group may be substituted with a substituent described above with respect to the alkyl group.

0072As non-limiting examples, the cycloalkyl group may be a cyclohexyl group, a cyclopentyl group, or the like. The cycloalkyl group may be unsubstituted or at least one hydrogen atom of the cycloalkyl group may be substituted with a substituent described above with respect to the alkyl group.

0073An embodiment of the present invention also provides a polymer of the naphthoxazine benzoxazine-based monomer of Formula 1.

0074The polymer can be prepared by dissolving the naphthoxazine benzoxazine-based monomer of Formula 1 in a solvent, and then polymerizing the resultant by a heat treatment, such as, for example, a heat treatment at a temperature range of 180 to 250° C. When the heat treatment temperature is less than 180° C., reactivity of polymerization may be degraded. On the other hand, when the heat treatment temperature is greater than 250° C., an unreacted compound may be produced so that the product yield may be reduced.

0075In this reaction, a polymerization catalyst, and the like can be used, if necessary.

0076The solvent used in the polymerization reaction may be N-methylpyrrolidone (NMP), dimethylacetamide (DMAc), or the like, and the amount of the solvent may be in the range of 5 to 30 parts by weight based on 100 parts by weight of the naphthoxazine benzoxazine-based monomer of Formula 1.

0077An embodiment of the present invention also provides a polymer that is a polymerization product of the naphthoxazine benzoxazine-based monomer of Formula 1 and a crosslinkable compound.

0078The crosslinkable compound may be at least one of polybenzimidazole, a polybenzimidazole-base complex, polybenzthiazole, polybenzoxazole and polyimide.

0079The amount of the crosslinkable compound may be in the range of 5 to 95 parts by weight based on 100 parts by weight of the naphthoxazine benzoxazine-based monomer of Formula 1.

0080When the polymer of the naphthoxazine benzoxazine-based monomer of Formula 1 according to aspects of the present invention is used in forming an electrode for a fuel cell, oxygen transmission is improved even when only air is supplied to a cathode, and wettability of phosphoric acid (H₃PO₄) in an electrode and thermal stability can be improved.

0081In addition, when the polymer of the naphthoxazine benzoxazine-based monomer is used in forming an electrolyte membrane for a fuel cell, thermal stability and durability of the electrolyte membrane at an operating temperature are improved.

0082Therefore, a fuel cell employing the electrode and an electrolyte membrane can operate at a high temperature under nonhumidified conditions, can have enhanced thermal stability, and can exhibit improved electricity generation performance.

0083The electrode for a fuel cell, according to aspects of the present invention includes a catalyst layer comprising a polymerization product of the naphthoxazine benzoxazine-based monomer of Formula 1 or a polymer of the naphthoxazine benzoxazine-based monomer of Formula 1 and a crosslinkable compound. The catalyst layer includes a catalyst. The polymer of the naphthoxazine benzoxazine-based monomer represented by Formula 1 may be used as a binder of the electrode, and in particular, can act as a binder. Thus, a commonly used binder is not necessary for the electrode.

0084The polymer of the naphthoxazine benzoxazine-based monomer of Formula 1 is a material that improves wettability of phosphoric acid. The amount of the polymer may be in the range of 0.1 to 65 parts by weight based on 100 parts by weight of the catalyst. When the amount of the polymer of the naphthoxazine benzoxazine-based monomer of Formula 1 is less than 0.1 parts by weight based on 100 parts by weight of the catalyst, wettability of phosphoric acid in an electrode may be insufficiently improved. On the other hand, when the amount of the polymer of the naphthoxazine benzoxazine-based monomer of Formula 1 is greater than 65 parts by weight based on 100 parts by weight of the catalyst, membrane forming properties may be decreased.

0085The catalyst may be platinum alone, or an alloy or mixture of platinum and at least one metal selected from the group consisting of gold, palladium, rhodium, iridium, ruthenium, tin, molybdenum, cobalt, and chrome. Alternatively, the catalyst may be a support catalyst in which the catalyst metal is loaded on a carbonaceous support. In particular, the catalyst may be a catalyst metal including at least one of Pt, PtCo, and PtRu, or a support catalyst in which the catalyst metal is loaded on a carbonaceous support.

0086The electrode may further include a binder that can be conventionally used in the preparation of an electrode for a fuel cell.

0087As non-limiting examples, the binder may be at least one selected from the group consisting of poly(vinylidenefluoride), polytetrafluoroethylene, tetrafluoroethylene-hexafluoropropylene copolymer, and perfluoroethylene. The amount of the binder may be in the range of 0.1 to 50 parts by weight based on 100 parts by weight of the catalyst. When the amount of the binder is less than 0.1 parts by weight based on 100 parts by weight of the catalyst, the adhesion between electrodes may be so poor that it may be difficult to maintain the shape of a catalyst layer. On the other hand, when the amount of the binder is greater than 50 parts by weight based on 100 parts by weight of the catalyst, an electric resistance in the electrode may be increased.

0088The type and amount of the crosslinkable compound may be the same as described above.

0089A method of preparing the electrode for a fuel cell described above is as follows.

0090First, a catalyst is dispersed in a solvent to obtain a dispersion. The solvent used may be N-methylpyrrolidone (NMP), dimethylformamide (DMAc), or the like, and the amount of the solvent may be in the range of 100 to 1,000 parts by weight based on 100 parts by weight of the catalyst.

0091A mixture of the naphthoxazine benzoxazine-based monomer of Formula 1 and a solvent is added to the dispersion and mixed together, and then the resultant is stirred. The mixture may further include a binder and a crosslinkable compound. The solvent may be N-methylpyrrolidone (NMP), dimethylacetamide (DMAc), or the like.

0092The resultant is coated on the surface of a carbon support to prepare an electrode. The carbon support may be fixed on a glass substrate in order to easily coat the resultant thereon. The coating method is not particularly limited, but, may be coating using a doctor blade, bar coating, screen printing, or the like.

0093The coated resultant is dried at a temperature in the range of 20 to 150° C., to remove the solvent. The drying time is dependent on the drying temperature, and may be in the range of 10 to 60 minutes.

0094As can be seen in the method of preparing an electrode described above, the electrode for a fuel cell contains a polymer of the naphthoxazine benzoxazine-based monomer of Formula 1. The naphthoxazine benzoxazine-based monomer of Formula 1 is polymerized during the drying process described above and/or while a fuel cell including the electrode operates.

0095If a crosslinking agent is further added to the mixture of the naphthoxazine benzoxazine-based monomer, the solvent, and the binder, the prepared electrode includes a polymer of the benzoxazine-based monomer and the crosslinking agent.

0096Hereinafter, an electrolyte membrane and a method of preparing the electrolyte membrane according to an embodiment of the present invention will be described. An electrolyte membrane formed using a crosslinkable compound is described herein. However, when an electrolyte membrane is prepared only using the naphthoxazine benzoxazine-based monomer of Formula 1, the preparation process is the same as that described herein, except that the crosslinkable compound is not used.

0097As a first method, the naphthoxazine benzoxazine-based monomer represented by Formula 1 may be blended with a crosslinkable compound, and the mixture is cured at a temperature in the range of 50 to 250° C., or more specifically, 80 to 220° C. The cured mixture is impregnated with a proton conductor such as an acid to prepare an electrolyte membrane.

0098The cross-linkable compound may be at least one selected from polybenzimidazoles (PBI), polybenzimidazole-base complexes, polybenzthiazoles, polybenzoxazoles, and polyimides. For example, polybenzimidazole-base complexes are disclosed in Korean Patent No. 2007-102579.

0099The amount of the crosslinkable compound may be in the range of 5 to 95 parts by weight based on 100 parts by weight of the naphthoxazine benzoxazine-based monomer of Formula 1. When the amount of the crosslinkable compound is less than 5 parts by weight, phosphoric acid may not be sufficiently impregnated. On the other hand, when the amount of the crosslinkable compound is greater than 95 parts by weight, the crosslinked object may be partially dissolved in a polyphosphoric acid in the presence of an excessive amount of phosphoric acid.

0100As a second method, an electrolyte membrane may be formed using a mixture of the naphthoxazine benzoxazine-based monomer represented by Formula 1 and a crosslinkable compound.

0101The formation of the electrolyte membrane may be performed by a tape casting method, or a conventional coating method. The conventional coating method may be a method in which the mixture is cast onto a support using a doctor blade. Herein, a doctor blade with a 250 to 500 μm gap may be used.

0102When the casting method using a doctor blade is used, the process of forming the electrolyte membrane further includes separating the electrolyte membrane from the support, between the time when curing of the mixture occurs and the time when impregnation of the resultant with acid occurs. To separate the electrolyte membrane from the support, the mixture is immersed in distilled water at temperature range of 60 to 80° C.

0103The support can be any support that can support an electrolyte membrane, such as, for example, a glass substrate, a polyimide film, and the like. When the tape casting method is used, a tape cast membrane is separated from a support such as polyethyleneterephthalate before being cured, and then put into an oven.

0104In addition, when a membrane is formed by the tape casting method using a mixture of a benzoxazine-based monomer and polybenzimidazole, a process of filtering the mixture may be further performed.

0105The tape cast membrane is cured by heat treatment, and then is impregnated with a proton conductor such as acid to form an electrolyte membrane.

0106Non-restrictive examples of the proton conductor include a phosphoric acid, and a C₁-C₂₀organic phosphonic acid. As non-limiting examples, the C₁-C₂₀organic phosphonic acid may be methyl phosphonic acid or ethyl phosphonic acid.

0107The amount of the proton conductor may be in the range of 300 to 1,000 parts by weight based on 100 parts by weight of the total weight of the electrolyte membrane. The concentration of the acid used is not particularly limited. As a non-limiting example, if phosphoric acid is used as the proton conductor, a 85 wt % aqueous phosphoric acid solution may be used, and the impregnation time of the phosphoric acid may be in the range of 2.5 to 14 hours at 80° C.

0108A method of preparing a fuel cell using the electrode for a fuel cell according to an embodiment of the present invention will now be described.

0109Any electrolyte membrane that is commonly used in the preparation of fuel cells can be used herein. For example, the electrolyte membrane that is commonly used in a fuel cell may be a polybenzimidazole electrolyte membrane, a polybenzoxazine-polybenzimidazole copolymer electrolyte membrane, a PTFE porous membrane, or the like.

0110Alternatively, an electrolyte membrane including a crosslinked product prepared by polymerization of the naphthoxazine benzoxazine-based monomer represented by Formula 1 and a crosslinkable compound may be used.

0111In particular, performance of the fuel cell including the electrode as described herein may be maximized by using the electrolyte membrane including the polymer that is a crosslinked product prepared by polymerization of the naphthoxazine benzoxazine-based monomer represented by Formula 1 and a crosslinkable compound.

0112A method of preparing a membrane-electrode assembly for a fuel cell, according to aspects of the present invention, is as follows. The term “membrane and electrode assembly (MEA)” used herein refers to a structure in which electrodes, each comprising a catalyst layer and a diffusion layer, are deposited on respective surfaces of the electrolyte membrane.

0113The MEA may be formed by positioning the electrodes each including the catalyst layer for an electrode described above at respective sides of the electrolyte membrane, joining the electrolyte membrane and electrodes together at a high temperature and a high pressure, and then joining a fuel diffusion layer to the catalyst layers.

0114Herein, the joining is performed under a pressure in the range of 0.1 to 3 ton/cm², or more specifically, at a pressure of about 1 ton/cm², in a state reached when the MEA is heated up to a temperature that softens the electrolyte membrane.

0115Next, a bipolar plate is disposed on each side of the membrane-electrode assembly to prepare a fuel cell. The bipolar plate has grooves used for supplying fuel, and functions as a current collector.

0116The use of the fuel cell according to aspects of the present invention is not particularly limited. For example, the fuel cell may be used as a polymer electrolyte membrane (PEM) fuel cell.

0117Hereinafter, aspects of the present invention will be described more specifically with reference to the following examples. The following examples are only for illustrative purposes and are not intended to limit the scope of the invention.

SYNTHESIS EXAMPLE 1

Preparation of 16DHN-3AP represented by Formula 6

01183.0 g of 1,6-dihydroxynaphthalene (18.7 mmol), 2.6 g of para-formaldehyde (82.4 mmol), and 3.88 g of 3-aminopyridine (41.2 mmol) were sequentially added to a 100 ml one-neck round bottomed flask, and then mixed in an oil bath at 90° C.

0119The reaction mixture was transparent in an early stage of the reaction, and about 30 minutes after the reaction, the reaction mixture was converted into a dark brown material in the form of a transparent gel. The reaction mixture was quenched with tetrahydrofurane (THF) to be cooled to room temperature. The crude product cooled to room temperature was base washed twice by solvent extraction using an aqueous 1N NaOH solution, and then washed once again with deionized water.

0120After the washing process was terminated, an organic layer was dried using MgSO₄, and then continuously filtered. The filtered solution was removed using a rotary evaporator, and then the purified product was dried in a vacuum oven at 40° C. for 6 hours to obtain the target material.

0121<figref idref="DRAWINGS">FIG. 4</figref> shows the nuclear magnetic resonance (NMR) spectrum of the target material prepared in Synthesis Example 1. The structure of the target material was confirmed by its NMR spectrum as shown in <figref idref="DRAWINGS">FIG. 4</figref>.

SYNTHESIS EXAMPLE 2

Preparation of 27DHN-34DFA represented by Formula 7

0122A target material was prepared in the same manner as in Synthesis Example 1, except that 14.41 g of 2,7-dihydroxynaphthalene (0.09 mmol), 12.33 g of para-formaldehyde (0.39 mmol), and 25 g of 3,4-difluoroaniline (0.194 mmol) were added to a 100 ml one-neck round bottom flask instead of the materials described in Synthesis Example 1.

0123<figref idref="DRAWINGS">FIG. 5</figref> shows the NMR spectrum of the target material prepared in Synthesis Example 2. The structure of the target material was confirmed by its NMR spectrum as shown in <figref idref="DRAWINGS">FIG. 5</figref>.

SYNTHESIS EXAMPLE 3

Preparation of 27DHN-2AP represented by Formula 8

0124A target material was prepared in the same manner as in Synthesis Example 1, except that 3.0 g of 2,7-dihydroxynaphthalene (18.7 mmol), 2.6 g of para-formaldehyde (82.4 mmol), and 3.88 g of 2-aminopyridine (41.2 mmol) were added to a 100 ml one-neck round bottom flask instead of the materials described in Synthesis Example 1.

0125<figref idref="DRAWINGS">FIG. 6</figref> shows the NMR spectrum of the target material prepared in Synthesis Example 3. The structure of the target material was confirmed by its NMR spectrum as shown in <figref idref="DRAWINGS">FIG. 6</figref>.

SYNTHESIS EXAMPLE 4

Preparation of 16DHN246TFA represented by Formula 9

0126A target material was prepared in the same manner as in Synthesis Example 1, except that 6.06 g of 2,4,6-trifluoroaniline (41.2 mmol) was used instead of 3.88 g of 3-aminopyridine (41.2 mmol).

0127<figref idref="DRAWINGS">FIG. 7</figref> shows the NMR spectrum of the target material prepared in Synthesis Example 4. The structure of the target material was confirmed by its NMR spectrum as shown in <figref idref="DRAWINGS">FIG. 7</figref>.

SYNTHESIS EXAMPLE 5

Preparation of 15DHN3AP represented by Formula 10

0128A target material was prepared in the same manner as in Synthesis Example 1, except that 3.0 g of 1,5-dihydroxynaphthalene (18.7 mmol), 2.6 g of para-formaldehyde (82.4 mmol), and 3.88 g of 3-aminopyridine (41.2 mmol) were added to a 100 ml one-neck round bottom flask instead of the materials described in Synthesis Example 1.

0129The structure of the target material was confirmed by the nuclear magnetic resonance (NMR) spectrum illustrated in <figref idref="DRAWINGS">FIG. 8</figref>.

SYNTHESIS EXAMPLE 6

Preparation of 27DHN246TFA represented by Formula 11

0130A target material was prepared in the same manner as in Synthesis Example 1, except that 3.0 g of 2,7-dihydroxynaphthalene (18.7 mmol), 2.6 g of para-formaldehyde (82.4 mmol), and 6.06 g of 2,4,6-trifluoroaniline (41.2 mmol) were added to a 100 ml one-neck round bottom flask.

0131The structure of the target material was confirmed by the NMR spectrum illustrated in <figref idref="DRAWINGS">FIG. 9</figref>.

REFERENCE EXAMPLE 1

Preparation of t-BuPh-a

013215 g of t-butylphenol (0.1 mol), 6.31 g of para-formaldehyde (0.21 mol), and 10.24 g of aniline (0.11 mol) were sequentially added in a 100 ml one-neck round bottom flask, and then mixed in an oil bath at 90° C.

0133The reaction mixture was opaque in an early stage of the reaction, and about 30 minutes after the reaction, the reaction mixture was converted into a dark brown material in the form of a transparent gel. The reaction mixture was quenched with tetrahydrofurane (THF) to be cooled to room temperature.

0134The crude product cooled to room temperature was base washed twice by solvent extraction using an aqueous 1N NaOH solution, and then washed once again with deionized water. After the washing process was terminated, an organic layer was dried using MgSO₄, and then continuously filtered. The solvent was removed from the filtered solution using a rotary evaporator, and then the purified product was dried in a vacuum oven at 40° C. for 6 hours to obtain t-BuPh-a.

0135The structure of t-BuPh-a was confirmed by its NMR spectrum.

0136Thermal stabilities of the compound of Synthesis Example 1, the compound of Synthesis Example 4, and t-BuPh-a of Reference Example 1 were evaluated using thermogravimetric analysis (TGA). <figref idref="DRAWINGS">FIG. 1</figref> is a graph showing thermogravimetric analysis (TGA) results of the compound prepared in Synthesis Example 1, the compound prepared in Synthesis Example 4, and t-BuPh-a prepared in Reference Example 1. In <figref idref="DRAWINGS">FIG. 1</figref>, thermogravimetric loss was measured at 800° C.

0137Referring to <figref idref="DRAWINGS">FIG. 1</figref>, it was confirmed that the compound of Formula 6 of Synthesis Example 1 and the compound of Formula 9 of Synthesis Example 4 had less thermogravimetric loss at a temperature of 800° C. or more than did t-BuPh-a. From the result, it can be seen that the compound of Formula 6 and the compound of Formula 9 have excellent thermal stability compared to t-BuPh-a.

SYNTHESIS EXAMPLE 7

Preparation of polymer of 16DHN3AP and PBI

013865 parts by weight of 16DHN3AP and 35 parts by weight of polybenzimidazole (PBI) were blended together, and the mixture was cured at a temperature in the range of about 180-240° C. to obtain a polymer of 16DHN3AP and PBI.

SYNTHESIS EXAMPLE 8

Preparation of polymer of 27DHN34DFA and PBI

013965 parts by weight of 27DHN34DFA and 35 parts by weight of polybenzimidazole (PBI) were blended together, and the mixture was cured at a temperature in the range of about 180-240° C. to obtain a polymer of 27DHN34DFA and PBI.

0140Thermal stabilities of 16DHN3AP, 27DHN34DFA, and the polymer of 16DHN3AP and PBI and the polymer of 27DHN34DFA and PBI that were prepared in Synthesis Examples 7 and 8, were evaluated using thermogravimetric analysis (TGA). The results are respectively shown in <figref idref="DRAWINGS">FIGS. 10 and 11</figref>. In <figref idref="DRAWINGS">FIGS. 10 and 11</figref>, thermogravimetric loss was measured at 800° C.

0141Referring to <figref idref="DRAWINGS">FIGS. 10 and 11</figref>, it can be seen that 16DHN3AP, 27DHN34DFA, and the polymer of 16DHN3AP and PBI and the polymer of 27DHN34DFA and PBI that were prepared in Synthesis Examples 7 and 8 have excellent thermal stability.

0142The structure of the solid-phase polymer of 27DHN34DFA and PBI was identified by its solid nuclear magnetic resonance (NMR) spectrum as shown in <figref idref="DRAWINGS">FIG. 16</figref>. The NMR spectroscopy was performed using a Varian Unity INOVA600 at 600 MHz.

EXAMPLE 1

Preparation of electrode for fuel cell and fuel cell including the electrode

01431 g of a catalyst in which 50 wt % of PtCo was supported on carbon and 3 g of NMP were added in a stirrer, and the mixture was stirred using a mortar to prepare a slurry. An NMP solution of 27DHN-34DFA of Formula 7 of Synthesis Example 2 was added to the slurry so that the resultant contained 0.025 g of 27DHN-34DFA. The resultant was further stirred.

0144Subsequently, an NMP solution of 5 wt % of polyvinylidenefluoride was added to the resultant so that the resultant contained 0.025 g of polyvinylidenefluoride. The resultant was mixed for 10 minutes to prepare a slurry used to form a cathode catalyst layer.

0145Carbon paper was cut to a size of 4×7 cm², fixed on a glass plate, and coated by a doctor blade (Sheen instrument). The gap interval was adjusted to 600 μm.

0146The slurry used to form a cathode catalyst layer was coated onto the carbon paper, and the resultant was dried at room temperature for 1 hour, dried at 80° C. for 1 hour, dried at 120° C. for 30 minutes, and dried at 150° C. for 15 minutes to prepare a cathode (a fuel electrode). The loading amount of PtCo in the prepared cathode was 2.1 mg/cm².

0147An electrode prepared by the following processes was used as an anode.

01482 g of a catalyst in which 50 wt % of Pt was supported on carbon and 9 g of NMP were added to a stirrer, and the mixture was stirred for 2 minutes using a high speed stirrer.

0149Subsequently, a solution in which 0.05 g of polyvinylidenefluoride was dissolved in 1 g of NMP was added to the mixture, and the resultant was further stirred for 2 minutes to prepare a slurry used to form an anode catalyst layer. The slurry used to form an anode catalyst layer was coated onto carbon paper coated with a microporous layer using a bar coater. As a result, preparation of the anode was completed. The loading amount of Pt in the prepared anode was 1.3 mg/cm².

0150Separately, 60 parts by weight of a benzoxazine-based monomer represented by Formula 12 below, 3 parts by weight of a benzoxazine-based monomer represented by Formula 13 below, and 37 parts by weight of polybenzimidazole were blended together, and then the mixture was cured at about 220° C.

0151<chemistry id="CHEM-US-00015" num="00015"><img file="US8551669B2_D0013.tif" /></chemistry>

0152Subsequently, the resultant was impregnated with 85 wt % of phosphoric acid at 80° C. for over 4 hours to form an electrolyte membrane. The amount of phosphoric acid was about 480 parts by weight based on 100 parts by weight of the total weight of the electrolyte membrane.

0153The electrolyte membrane was disposed between the cathode and the anode to prepare a MEA. The cathode and anode were not impregnated with phosphoric acid.

0154To prevent gas permeation between the cathode and the anode, a TEFLON membrane for a main gasket with a thickness of 200 μm and a TEFLON membrane for a subgasket with a thickness of 20 μm were joined and disposed between the electrode and the electrolyte membrane. The pressure applied to the MEA was adjusted to 1, 2, 3 N-m torque step by step using a wrench to assemble a cell.

0155Electricity was generated by causing hydrogen to flow into the anode (flowrate: 100 ccm) and causing air to flow into the cathode (flowrate: 250 ccm) at 150° C. under a condition in which the electrolyte membrane was not humidified. Properties of the fuel cell prepared were measured. An electrolyte doped with a phosphoric acid was used, and thus the performance of the fuel cell improved as time elapsed. Aging was performed until an operating voltage reached a peak, and then the properties of the fuel cell were finally evaluated. In addition, the area of the cathode and anode was fixed to a size of 2.8×2.8 (7.84 cm²), and the thickness of the cathode was about 430 μm and the thickness of the anode was about 390 μm, although the thicknesses of the cathode and the anode may have varied according to the distribution of the carbon paper.

EXAMPLE 2

Preparation of Electrode for Fuel Cell and Fuel Cell Including the Electrode

0156A cathode was prepared in the same manner as in Example 1, except that 16DHN-3AP of Formula 6 of Synthesis Example 1 was used instead of 27DHN-34DFA of Formula 7 of Synthesis Example 2, and a fuel cell using the cathode was prepared.

EXAMPLES 3-5

Preparation of Electrode for Fuel Cell and Fuel Cell Including the Electrode

0157Cathodes were prepared in the same manner as in Example 1, except that 27DHN-2AP of Formula 8 of Synthesis Example 3, 16DHN246TFA of Formula 9 of Synthesis Example 4, and 15DHN3AP of Formula 10 of Synthesis Example 5, respectively were used instead of 27DHN-34DFA of Formula 7 of Synthesis Example 2, and fuel cells using the cathodes were prepared.

COMPARATIVE EXAMPLE 1

Preparation of Electrode for Fuel Cell and Fuel Cell Including the Electrode

0158A cathode was prepared in the same manner as in Example 1, except that 27DHN-34DFA of Formula 7 of Synthesis Example 2 was not used, and a fuel cell using the cathode was prepared.

0159<figref idref="DRAWINGS">FIG. 2</figref> is a graph showing a change in voltage with respect to time of fuel cells prepared in Example 1 and Comparative Example 1.

0160Referring to <figref idref="DRAWINGS">FIG. 2</figref>, although the fuel cell of Example 1 had low initial performance, it had improved voltage performance by faster activation compared to the fuel cell of Comparative Example 1.

0161In addition, changes in cell potential with respect to current density of the fuel cells of Examples 1 and 2 and Comparative Example 1 were measured, and the results are shown in <figref idref="DRAWINGS">FIG. 3</figref>.

0162Referring to <figref idref="DRAWINGS">FIG. 3</figref>, the fuel cells of Examples 1 and 2 had higher cell voltage characteristics compared to the fuel cell of Comparative Example 1.

0163Cell performances of the fuel cells of Examples 1 through 5 and Comparative Example 1 were measured, and the results are shown in Table 1 below.

0164<tables id="TABLE-US-00001" num="00001"><table frame="none" colsep="0" rowsep="0"><tgroup align="left" colsep="0" rowsep="0" cols="3"><colspec colname="offset" colwidth="112pt" align="left" /><colspec colname="1" colwidth="49pt" align="center" /><colspec colname="2" colwidth="56pt" align="center" /><thead><row><entry /><entry namest="offset" nameend="2" rowsep="1">TABLE 1</entry></row><row><entry /><entry namest="offset" nameend="2" align="center" rowsep="1" /></row><row><entry /><entry>Voltage at</entry><entry>Tafel slope</entry></row><row><entry /><entry>0.3 A/cm²(V)</entry><entry>(mV/dec)</entry></row><row><entry /><entry namest="offset" nameend="2" align="center" rowsep="1" /></row></thead><tbody valign="top"><row><entry /></row></tbody></tgroup><tgroup align="left" colsep="0" rowsep="0" cols="4"><colspec colname="offset" colwidth="14pt" align="left" /><colspec colname="1" colwidth="98pt" align="left" /><colspec colname="2" colwidth="49pt" align="center" /><colspec colname="3" colwidth="56pt" align="char" char="." /><tbody valign="top"><row><entry /><entry>27DHN-34DFA (Example 1)</entry><entry>0.685</entry><entry>98</entry></row><row><entry /><entry>16DHN-3AP (Example 2)</entry><entry>0.685</entry><entry>99</entry></row><row><entry /><entry>27DHN-2AP (Example 3)</entry><entry>0.686</entry><entry>104</entry></row><row><entry /><entry>16DHN246TFA (Example 4)</entry><entry>0.688</entry><entry>104</entry></row><row><entry /><entry>15DHN3AP (Example 5)</entry><entry>0.684</entry><entry>108</entry></row><row><entry /><entry>Comparative Example 1</entry><entry>0.678</entry><entry>97</entry></row><row><entry /><entry namest="offset" nameend="3" align="center" rowsep="1" /></row><row><entry /><entry namest="offset" nameend="3" align="left" id="FOO-00001">Referring to Table 1, the fuel cells of Examples 1 through 5 have a higher Tafel slope and improved voltage characteristics compared to the fuel cell of Comparative Example 1.</entry></row></tbody></tgroup></table></tables>

EXAMPLE 6

Preparation of an Electrolyte Membrane for a Fuel Cell and a Fuel Cell Using the Electrolyte Membrane

01651 g of a catalyst in which 50% by weight of PtCo was loaded on carbon and 3 g of NMP as a solvent were added to a stirrer, and the mixture was agitated using a mortar to prepare a slurry.

0166Then, a solution of 5% by weight of polyvinylidenefluoride and NMP was added to the mixture to set the amount of the polyvinylidenefluoride to 0.025 g, and the mixture was mixed for 10 minutes to prepare a slurry for a cathode catalyst layer.

0167Carbon paper was cut into pieces of 4×7 cm²in size, and the pieces were fixed on a glass plate and coated using a doctor blade (Sheen instrument), wherein the gap interval of the doctor blade was 600 μm.

0168The slurry for a cathode catalyst layer was coated onto the carbon paper and dried at room temperature for 1 hour, at 80° C. for 1 hour, at 120° C. for 30 minutes and at 150° C. for 15 minutes to prepare a cathode (a fuel electrode). The amount of loaded Pt/Co in the prepared cathode was 2.32 mg/cm².

0169An electrode prepared according to the process as follows was used as an anode.

01702 g of a catalyst in which 50% by weight of Pt is supported on carbon and 9 g of NMP solvent were added to a stirrer and the mixture was agitated in a high-speed agitator for 2 minutes.

0171Then, a solution of 0.05 g of polyvinylidenefluoride dissolved in 1 g of NMP was added thereto and agitated for 2 minutes to prepare a slurry for an anode catalyst layer. The slurry was coated onto carbon paper on which microporous layer was coated using a bar coater. The amount of loaded Pt in the prepared anode was 1.44 mg/cm².

0172Separately, 65 parts by weight of 27DHN-34DFA of Formula 7 prepared in Synthesis Example 2 was blended with 35 parts by weight of polybenzimidazole (PBI), and the mixture was cured at about 220° C.

0173Then, the resultant was impregnated with 85% by weight of phosphoric acid at 80° C. for more than 4 hours to prepare an electrolyte membrane. The amount of phosphoric acid was about 530 parts by weight based on 100 parts by weight of electrolyte membrane.

0174A membrane electrode assembly (MEA) was prepared by interposing the electrolyte membrane between the cathode and the anode. The cathode and anode were not impregnated with phosphoric acid.

0175A 200 μm TEFLON membrane for a main gasket and a 20 μm TEFLON membrane for a sub gasket were overlapped on an interface between the electrodes and electrolyte membrane in order to prevent gas permeation between the cathode and the anode. The pressure applied to the MEA was adjusted to 1, 2, 3 N-m torque step by step using a wrench to assemble a cell.

0176Characteristics of fuel cells were measured while operating by supplying hydrogen to the anode at 100 ccm and supplying air to the cathode at 250 ccm at 150° C. while the electrolyte membrane was not hydrated. Since cell efficiency increases with time by using the electrolyte doped with phosphoric acid, the final efficiency was measured after the fuel cell was aged until operational voltage was maximized. The area of the cathode and the anode was fixed to 2.8×2.8=7.84 cm², and the thickness of the cathode was about 430 μm and the thickness of the anode was about 390 μm although the thicknesses of the cathode and the anode may have varied according to the distribution of the carbon paper.

EXAMPLES 7 TO 9

Preparation of an Electrolyte Membrane for a Fuel Cell and a Fuel Cell Using the Electrolyte Membrane

0177An electrolyte membrane and a fuel cell were prepared in the same manner as in Example 6, except that 27DHN-246DFA, 16DHN-34DFA, and 16DHN-3AP were respectively used instead of 27DHN-34DFA of Formula 7 prepared in Synthesis Example 2.

0178Voltage characteristics according to current density of the fuel cell prepared in Example 6 were measured, and the results are shown in <figref idref="DRAWINGS">FIG. 12</figref>. In <figref idref="DRAWINGS">FIG. 12</figref>, “OCV” denotes an open circuit voltage, and “0.2 A/cm²” denotes cell voltage at a current density of 0.2 A/cm².

0179Referring to <figref idref="DRAWINGS">FIG. 12</figref>, the fuel cell of Example 6 had an open circuit voltage of more than 1 V and 0.72 V at 0.2 A/cm².

0180In addition, a change in cell voltage according to time was measured, and the results are shown in <figref idref="DRAWINGS">FIG. 13</figref>.

0181Referring to <figref idref="DRAWINGS">FIG. 13</figref>, the fuel cell of Example 6 showed excellent cell voltage characteristics.

0182Conductivity according to temperature and phosphoric acid doping level of the electrolyte membranes prepared in Examples 6 through 9 was measured, and the results are shown in <figref idref="DRAWINGS">FIGS. 14 and 15</figref>.

0183Referring to <figref idref="DRAWINGS">FIGS. 14 and 15</figref>, the electrolyte membranes of Examples 6 through 9 showed higher conductivity compared with the PBI electrolyte membrane, and showed good durability due to a small doping amount of phosphoric acid.

0184In <figref idref="DRAWINGS">FIG. 15</figref>, the doping level is shown as a percentage based on the weight of the impregnated amount.

EXAMPLE 10

Preparation of a Fuel Cell

0185A fuel cell was prepared in the same manner as in Example 6, except that the slurry for a cathode catalyst layer was prepared in the following processes.

01861 g of a catalyst in which 50% by weight of PtCo was loaded on carbon and 3 g of NMP as a solvent were added to a stirrer, and the mixture was agitated using a mortar to prepare a slurry. An NMP solution of 27DHN-34DFA of Formula 7 prepared in Synthesis Example 2 was then added to the slurry so that the resultant contained 0.025 g of 27DHN-34DFA. The resultant was further stirred.

0187Then, a solution of 5% by weight of polyvinylidenefluoride and NMP was added to the mixture to set the amount of the polyvinylidenefluoride to 0.025 g, and the mixture was mixed for 10 minutes to prepare a slurry for a cathode catalyst layer.

COMPARATIVE EXAMPLE 2

Preparation of Fuel Cell

0188A fuel cell was prepared in the same manner as in Example 10, except that 27DHN-34DFA of Formula 7 was not used in the preparation of the cathode and a polybenzimidazole (PBI) membrane was used as an electrolyte membrane.

0189Cell voltage characteristics with respect to current density of the fuel cells prepared in Example 10 and Comparative Example 2 were measured, and the results are shown in <figref idref="DRAWINGS">FIG. 17</figref>.

0190Referring to <figref idref="DRAWINGS">FIG. 17</figref>, performance of the MEA prepared in Example 10 was improved compared with that of the MEA prepared in Comparative Example 2.

0191While aspects of the present invention have been particularly shown and described with reference to differing embodiments thereof, it should be understood that these exemplary embodiments should be considered in a descriptive sense only and not for purposes of limitation. Descriptions of features or aspects within each embodiment should typically be considered as available for other similar features or aspects in the remaining embodiments.

0192Although a few embodiments of the present invention have been shown and described, it would be appreciated by those skilled in the art that changes may be made in this embodiment without departing from the principles and spirit of the invention, the scope of which is defined in the claims and their equivalents.